Drop in refrigerant blend for mineral oil based systems

ABSTRACT

The present disclosure relates to refrigerants generally, and more specifically to non-flammable, non-ozone depleting mixtures of refrigerants that may be substituted for (HCFC R-22, R-407C, R-417A, R-502, R-402A, R-402B, R-404A, R-408A &amp;R-507A) and usable in mineral oil systems. Among the most preferred embodiments of the present invention(s) are mixtures that are substitutes for these refrigerants, comprising about 35 to 65 weight percent R-125, and about 20 to 55 weight percent R-134a, and about 5 to 25 weight percent of R-143a and about 1 to 5 weight percent hydro component of (R-600 OR R-601) or combination, and about 2-10 weight percent of R-227ea the weight percentages of the components being weight percentages of the overall mixture.

CROSS REFERENCE TO RELATED APPLICATIONS

This Application is a continuation application and claims the benefit ofand priority under 35 U.S.C. 120 to U.S. patent application Ser. No.13/861,084 filed Apr. 11, 2013, entitled “Drop In Refrigerant Blend ForMineral Oil Based Systems,” by Ahmad M. Shihab, pending, to be issued asU.S. Pat. No. 8,652,348, which is hereby incorporated by referenceherein as if set forth herein in its entirety, which is a continuationof U.S. patent application Ser. No. 13/718,722, filed Dec. 18, 2012,entitled “Drop In Refrigerant Blend For Mineral Oil Based Systems,” byAhmad M. Shihab, which is hereby incorporated by reference herein as ifset forth herein in its entirety.

TECHNICAL FIELD

The present disclosure relates to refrigerant blends, and moreparticularly to nonflammable, nonozone depleting, mixtures ofrefrigerants that may be substituted for HCFC-22, R-407C, R-417A,R-402A, R-402B, R-404A, R-408A, R-502, and R-507A which is usable inmineral oil systems.

BACKGROUND

The U.S. Environmental Protection Agency and other world scientificbodies have determined that refrigerants comprising chlorofluorocarbons(CFCs) cause harm to the Earth's stratospheric ozone layer after beingreleased into the atmosphere. Hydrochlorofluorocarbons (HCFCs), whichare chlorofluorocarbons containing one or more hydrogen atoms, alsocause damage to the ozone layer but such damage is generally less thanthat caused by CFCs. Various rules, regulations, protocols and treatiesin the world have phased out CFCs, or are now doing so. HCFCs are beingallowed as “transition” substances between CFCs and various zero ozonedepletion alternatives. HCFCs are also under phase outs, but on a muchlonger time scale than the CFCs, with the final HCFC phase-out being inthe year 2030. Certain countries may phase out HCFCs earlier than 2030,and certain categories of use (e.g., production of new equipmentcontaining HCFCs) may be phased out earlier, as well, while othercategories of use (service fluids for repair of existing equipment) maybe maintained until 2030.

Several non-ozone depleting refrigerants have already been developed inthe prior art. However, most of them have one or more drawbacks. Themain drawback is that refrigerants comprised of hydrofluorocarbons(HFCs), or mixtures thereof, do not mix (are not miscible in) mineraloils used for the earlier CFC and HCFC refrigerants (e.g., CFC-12 andHCFC-22, R-502, R-500). R-407C, comprising R-32/125/134a (23/25/52),closely matches the pressure temperature curve of HCFC-22. However, itrequires ester (POE) oil and is totally non-miscible in mineral oil.Ester oils are far more expensive and are less stable than mineral oils.Ester oils also are far more hygroscopic than mineral oils, so moisturecan enter a refrigeration system much easier during manufacture orservice than it can with mineral oils. This moisture is extremelydamaging, and causes the refrigerants to slowly hydrolyze and decomposeinto hydrofluoric acid (HF) and other components leading to early systemfailures.

This disclosure relates generally to novel refrigerant blends that canbe used to replace chlorofluorocarbon (CFC) and hydrochlorofluorocarbon(HCFC) refrigerants. More particularly, the disclosure relates to novelrefrigerant blends that can be used to replace R-22(chlorodifluoromethane) in refrigeration systems designed to use R-22 asthe refrigerating fluid.

Refrigeration systems have been in widespread use for decades and have awide variety of uses, such as comfort cooling, household refrigeration,automobile air conditioning, commercial freezer cooling. Such systemswork on the basic premise that a fluid, known as a refrigerant, picks upheat from an area to be refrigerated, and disposes of the heat in anarea not adversely affected by an increase in heat. Typically,refrigeration processes encompass a changing state of the refrigerantfluid from a liquid to a vapor, and from a vapor to a liquid, whichchange of state allows for the rapid removal of heat from the area to berefrigerated. Different types of refrigeration systems use differentrefrigerants having properties designed to enable the given system toapproach peak performance.

Chlorofluorocarbon refrigerants such as R-12 (dichlorodifluoromethane)were the refrigerants of choice for many years in domestic andcommercial refrigeration, as well as in automobile air conditioners.However, in view of the recognition in the scientific community thatthese chlorine-containing refrigerants have an adverse effect on theearth's ozone layer, international agreements have mandated a phase-outof these refrigerants in favor of more environmentally friendlyrefrigerants. Hydrochlorofluorocarbon refrigerants such as R-22, whilebelieved to be less environmentally problematic than CFCs, are alsochlorine-containing, and have likewise raised concerns in the scientificcommunity. International agreements have called for a gradual phase-outof HCFC refrigerants.

Numerous low ozone-depleting refrigerants have been promoted asreplacement refrigerants. A widely used replacement refrigerant has beenR-134a (1,1,1,2tetrafluoroethane). R-134a contains no chlorine atoms,and is non-ozone-depleting, nonflammable and non-toxic. However, the useof R-134a necessitates major changes in most refrigeration systems. Forexample, the mineral oil lubricants typically used with CFC and HCFCrefrigerants are not compatible with R-134a. As a result, it isnecessary to completely drain this oil from systems previously using CFCand HCFC refrigerants, and replaces it with other lubricants that aremore compatible with R-134a, such as polyolester (POE) and polyalkyleneglycol (PAG) lubricants. In addition, some equipment used in existingair conditioning systems is not compatible with R-134a, thusnecessitating significant overhaul and replacement of portions of theseair conditioning systems

When new products are designed and/or put into service, such productscan be engineered for use with new refrigerants such as R-134a. Thus,such products can be manufactured with components that are compatiblewith R-134a, and can be produced for use with compatible lubricatingoils. However, the situation is more problematic when existingrefrigeration systems require replacement refrigerant. Replacements areoften required when, for example, existing refrigerant is leaked orevaporated from the system. Replacement refrigerant also must beperiodically added to such systems during routine maintenance of thesystem. In existing refrigeration systems, it is often cost prohibitiveto retrofit the system to be compatible with non-CFC or non-HCFCrefrigerants such as R-134a. In addition, in small systems it is ofteninconvenient and uneconomical to completely drain the existing lubricantand replace it with lubricating oil that is more compatible with areplacement refrigerant.

Several refrigerant compositions that are intended to replace R-22 arecommercially available. The three best known replacement refrigerantsare R-407C (a combination of R-134a, R-125, and R-32), R-410A (a binaryblend of R-125 and R-32) and R-417A (a blend of R-125, R-134a, andR-600). R-410A is a high pressure refrigerant that cannot be used inexisting R-22 equipment. As a result, the existing refrigerationequipment must be replaced when this refrigerant is used. R-407C can beused in existing R-22 systems; however, this refrigerant is notcompatible with the mineral oil lubricants used in such systems. As aresult, the system must be flushed, and the lubricant must be replacedwith one that is compatible. R-417 A can be used in existing R-22systems with existing oils. However, this refrigerant shows a decreasein refrigerating capacity about 5 to 15 percent when compared to R-22.

Thus, there is a long-felt but unresolved need for replacing a R-22refrigerant with a new refrigerant, without the necessity of drainingthe existing lubricant and/or overhauling the existing refrigerationequipment to make it compatible with the new refrigerant. Preferably,the replacement refrigerant would be low cost, have low flammability andtoxicity, have refrigerating capacity similar to the existingrefrigerant, be compatible with the existing system and lubricant, andhave the ability to substantially resist fractionation into flammablecomponents upon evaporation or leakage from the refrigeration system.

BRIEF SUMMARY OF THE DISCLOSURE

Briefly described, and according to one embodiment, aspects of thepresent disclosure generally relate to novel refrigerant compositionsthat may be used in place of CFC and HCFC refrigerants. The inventiverefrigerant compositions are a non-stratospheric ozone depletingalternative that can be used to replace R-22 refrigerants.

In particular, the inventive refrigerant composition meets at least thefollowing objectives:

-   -   1. To provide a solution for replacing R-22 refrigerant with a        non-stratospheric ozone depleting alternative.    -   2. To provide a solution for replacing R-502 refrigerant with a        non-stratospheric ozone depleting alternative.    -   3. To provide a solution for replacing R-404A refrigerant with        an alternative that uses lower cost and more stable mineral oil.    -   4. To provide a solution for replacing R-407C refrigerant with        an alternative that uses lower cost and more stable mineral oil.    -   5. To provide a solution for replacing R-417A refrigerant with        an alternative that uses mineral oil in a wider variety of        applications and provides much less loss of capacity than        R-417A.    -   6. To be compatible with lubricants and materials used in CFC        and HCFC systems (mineral and alkylbenzene oil).    -   7. To improve energy efficiency compared to R-22.    -   8. To reduce the compressor discharge temperatures compared to        R-22. This will allow higher compression ratios (lower suction        pressures and thus lower temperatures) than R-22. R-22 has a        very high heat of compression, which limits the maximum        compression ratios due to the need to keep compressor discharge        gas temperatures below about 300° F. to prevent breakdown of the        refrigerant and oil.    -   9. To be nonflammable, and to be able to pass a UL2182        flammability test to qualify for an ASHRAE designation of A1.

The preferred embodiments of the present disclosure are mixtures ofrefrigerants that are substitutes for chlorodifluoromethane (R-22)refrigerant, comprising about 35 to 65 weight percent R-125, and about20 to 55 weight percent R-134a, and about 5 to 25 weight percent ofR-143a and about 1 to 5 weight percent of (R-600 OR R-601 orcombination) and about 2-10 weight percent of R-227ea. The weightpercentages of the components being weight percentages of the overallmixture.

Other preferred mixture of refrigerants that is a substitute for R-502(48.8 weight percent chlorodifluoromethane and 51.2 weight percentchloropentafluoroethane) and R-404A (44 weight percentpentafluoroethane, 52 weight percent 1,1,1-trifluoroethane, and 4 weightpercent 1,1,1,2-tetrafluoroethane), R-402A, R-402B, R-404A, R-408A andR-507A refrigerants, comprising about 45 to 75 weight percentPentafluoroethane (HFC-125); and about 5 to 20 weight percent1,1,1,2-Tetrafluoroethane (HFC-134a); and about 10 to 40 weight percent1,1,1, Trifluoroethane (HFC-143a);) and about 1 to 5 weightN-Butane(R-600) or Isopentane (R-601a) or combination and about 2 to 10weight percent 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea) with theweight percentages of the components of the mixture being weightpercentages of the overall mixture.

These and other aspects, features, and benefits of the claimedinvention(s) will become apparent from the following detailed writtendescription of the preferred embodiments and aspects taken inconjunction with the following drawings, although variations andmodifications thereto may be effected without departing from the spiritand scope of the novel concepts of the disclosure.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a graphical chart showing exemplary power consumption (inunits of Watts) of various refrigerants.

FIG. 2 is a graphical chart showing average discharge pressures (inunits of psi) of various refrigerants.

FIG. 3 is a graphical chart showing exemplary capacities (in units ofBTUs/H) of various refrigerants.

FIG. 4 is a graphical chart showing exemplary efficiencies of variousrefrigerants.

DETAILED DESCRIPTION OF THE DISCLOSED EMBODIMENTS

For the purposes of promoting an understanding of the principles of theinvention, reference will now be made to the embodiments described belowand specific language will be used to describe the same. It willnevertheless be understood that no limitation of the scope of theinvention(s) is thereby intended, such alterations and furthermodifications in the described embodiments, and such furtherapplications of the principles of the invention(s) as described thereinbeing contemplated as would normally occur to one skilled in the art towhich the present disclosure relates.

The present disclosure teaches novel refrigerant blends comprising therefrigerants Pentafluoroethane (HFC-125); 1,1,1,2-Tetrafluoroethane(HFC-134a); 1,1,1, Trifluoroethane (HFC-143a);1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea); and {N-Butane(R-600) orIsopentane(R-601a) or both combination}. The refrigerant blends may beused in place of CFC and HCFC refrigerants, and particularly, may beused in place of refrigerant R-22. The inventive refrigerant blends aresubstantially non-toxic, non-ozone-depleting, compatible withrefrigeration compressor lubricating oils presently in use, and haverefrigerating properties that are substantially the same as, or betterthan, the properties of the refrigerant that it is replacing. Inaddition, the inventive refrigerant compositions are non-flammable; bothas originally placed in the refrigeration system, and after 99% of therefrigerant have leaked from the system. The inventive refrigerantblends utilize a unique combination of non-ozone depleting refrigerants.Components utilized in the inventive blend include R-125, R-134a,R-143a, R-227ea and hydrocarbon component (Either R-600 or R-601a orboth combination). In what follows next, two particularly preferredembodiments of the inventive refrigerant blend are described below. Thecomponents are identified, along with the proportions, by weight percentof the components in the overall refrigerant blend.

Blend 1: A Mixture of Refrigerants that is a Substitute for R-22,R-134a, R-417a and R-507C.

R-125 in an amount of about 35-65%; preferably 40-60%; more preferably50-57%, and most preferably 55%;

R-134a in an amount of about 20-55%; preferably 25-45%; more preferably27-35%, and most preferably 32%;

R-143a in an amount of about 5-25%; preferably 5-20%; more preferably6-10%, and most preferably 7%;

R-600 Or R-601a or combination of both hydrocarbons components in theamount of about 1-5%; preferably 2-4%; more preferably 2-3%, and mostpreferably 3%;

R-227ea in an amount of about 2-10%; preferably 2-8%; more preferably2-5%, and most preferably 3%;

Blend 2: A mixture of refrigerants that is a substitute for R-404A,R-502, R-22 R-402A, R-402B, R-404A, R-408A, and R-507A.

R-125 in an amount of about 45-75%; preferably 50-70%; more preferably55-68%, and most preferably 65%;

R-134a in an amount of about 5-20%; preferably 5-15%; more preferably6-10%, and most preferably 7%;

R-143a in an amount of about 10-40%; preferably 15-30%; more preferably20-28%, and most preferably 22%;

R-600 Or R-601a or combination of both hydrocarbons components amount ofabout 1-5%; preferably 2-4%; more preferably 2-3%, and most preferably3%;

R-227ea in an amount of about 2-10%; preferably 2-8%; more preferably2-5%, and most preferably 3%;

The proportions of each of the listed ingredients may be varied withinthe general ranges provided, as long as the variations are not sosubstantial that the benefits of the invention(s) cannot be achieved.The amounts of the components should not be varied in a manner such thatthe operating characteristics of the refrigeration system and/or theflammability, toxicity and ODP (ozone depleting potential) are adverselyaffected to any significant degree. Processes for mixing refrigerantcomponents to arrive at a refrigerant blend are well known in therefrigerant art, and no special techniques are required to prepare theinventive blends. It has been known that a small amount of a hydrocarboncomponent in a refrigerant blend can greatly increase the miscibility ofcompressor lubrication oils commonly found in refrigeration systems,such as R-22 systems. In some systems as little as 1% of a hydrocarboncomponent provides sufficient miscibility to enable satisfactory oilreturn to the compressor. When the concentration of the hydrocarboncomponent of the present refrigerant blend exceeds about 2.5% by weightof the total blend, the refrigerant has miscibility similar to that ofR-22 in mineral-based compressor lubricating oil.

The Hydrocarbon components N-butane have a boiling point (about 31° F.,−0.6° C.) and Isopentane have a boiling point (about 82° F., 27.8° C.)is higher than the evaporator temperature of most R-22 refrigeratingsystems such as air conditioning systems, where the evaporatortemperature is normally between about 25 and 30° F. (between −4 and I.I°C.). As refrigerant leaks out of the system or container, the percentageof N-butane and/or Isopentane in the liquid phase goes down therefrigerant remaining in each phase after leak out never exceeds theflammability limit.

To take advantage of the effects exhibited by certain hydrocarbons, acombination of components N-butane and Isopentane or combination of bothare selected such that the percentage of the hydrocarbon component inthe refrigerant blend does not appreciably change as refrigerant leaksout of the system, and therefore does not cause the hydrocarboncomponent of either the vapor or liquid phase to exceed the flammabilitylimit.

EXAMPLES Example 1 Performance Testing

The time required to reduce the air temperature inside an insulatedfreezer at a defined starting temperature provides a good estimate ofthe refrigerating capacity of a refrigerant blend, and also provides agood basis to compare the performance of the blend to the performance ofR-22 and other commercially available blends that are compatible with arefrigeration system.

A refrigerant blend according to the present invention(s) was preparedwith the following percentages (based on the weight of the entire blend)of components:

-   -   1. R-125a in an amount of 65 wt. %.    -   2. R-134a in an amount of 7 wt. %.    -   3. R-143a in an amount of 22 wt. %    -   4. R-600 in an amount of 1.5 wt. % AND R-601a in amount of 1.5        wt. %.    -   5. R-227ea in an amount of 3 wt. %.

A freezer made by True manufacturing (R-404A) system, 72 cubic footreach in has a 5550 BTU/h capacity was charged with the above blend. Therefrigeration system was connected to a scanner to record thetemperature inside the box and measure the discharge pressure of thecompressor and the power consumptions.

The refrigerant blend described above was charged in the testing unitand the system was continuously run to reduce the temperature in thecooling box from 60° F. {15.6° C. (Room Temperature)} to the lowestpossible temperature. The same procedure was followed for comparativerefrigerant blends R-404A, R-502A, R-22a and R-507A.

The test results are provided below:

TABLE 1 (Temperature drop for R-404a) Time (Min) Temp.° F. 0 60.39 1034.04 20 15.28 30 1.61 40 −6.4 50 −11.38 60 −14.51 70 −16.85 80 −18.4290 −19.68 100 −20.56 110 −21.25 120 −21.93 130 −22.32 140 −23.01

TABLE 2 (Temperature drop for R-502a) Time (Min) Temp.° F. 0 60.71 1040.58 20 23.29 30 10.3 40 0.44 50 −6.69 60 −11.58 70 −14.9 80 −17.15 90−18.81 100 −19.98 110 −20.86 120 −21.44 130 −21.93 140 −22.22 150 −22.42160 −23.01

TABLE 3 (Temperature drop for R-22a) Time (Min) Temp.° F. 0 60.46 1034.23 20 17.73 30 4.64 40 −5.13 50 −11.48 60 −15.68 70 −18.71 80 −20.5690 −21.93 100 −23.1

TABLE 4 (Temperature drop for R-507a) Time (Min) Temp.° F. 0 60.76 1037.46 20 19.09 30 5.13 40 −4.64 50 −10.8 60 −14.61 70 −17.44 80 −19.3990 −20.76 100 −21.83 110 −22.62 120 −23.3

TABLE 5 (Temperature drop for Refrigerant Blend. Time (Min) Temp.° F. 060.54 10 35.02 20 19.09 30 6.79 40 −2.2 50 −8.94 60 −13.14 70 −16.07 80−18.12 90 −19.88 100 −22.15 110 −23

From the above data (Tables 1-5) indicates it took 110 minutes to dropthe temperature inside the box from 60° F. to −23° F. when the inventedblend utilized; this is faster than tested comparable refrigerant blendslike R-404a, R-502A, R-507 and very close to R-22 temperature drop.

That concludes the inventive blend has better cooling capacity than anyother tested blends R-404a, R-502A and R-507.

Also the power consumption was measured during running the mentionedsystem for each refrigerant and the results are listed on Table 6 andFIG. 1:

TABLE 6 (power consumptions) Refrigerant Watts R-404A 1734.05 R-221670.42 R-507A 1700.65 R-502A 1714.93 Refrigerant 1679.96 Blend

Refrigerant blend consumed 179.96 watts which is lower than what otherrefrigerant consumed, this indicates that the refrigerant blend hasbetter efficiency compared to other tested blends like R-404a, R-502Aand R-507. Further more the compressor discharges pressures weremeasured after running 420 minutes and the results are listed on Table7, see FIG. 2.

TABLE 7 (Average Discharge Pressures) Average Discharge RefrigerantPressure (psi) R-404A 202.14 R-22 168.25 R-507A 195.5 R-502A 207.3Refrigerant Blend 171.64

The above test results indicate that the average discharge pressure forthe invented blend during the test period was 171.64 psi which is lowercompared to other test blends like R-404a, R-502A and R-507. Thisproperty is very essential to long lasting compressor life.

Example 2

Further performance testing was performed in insulated box utilizing aSamsung Split system air conditioner (Model 590ANX02) manufactured touse R-22 refrigerant. The evaporator placed inside the box (8′×10′×7′)(2.44 m×3.05 m×2.13 m.) and was lined with a 4-inch (10.2 cm.) layer ofpolyurethane. The air conditioner was connected to a scanner to recordthe temperature inside the box, total current AMPs and current voltageat any given minute to calculate the total BTUs and the efficiency(EER).

Tests were performed on a blend according to Blend 1 as determinedpreviously:

-   -   1. R-125a in an amount of 55 wt. %.    -   2. R-134a in an amount of 32 wt. %.    -   3. R-143a in an amount of 7 wt. %    -   4. R-600 in an amount of 1.5 wt. % AND R-601a in amount of 1.5        wt. %.    -   5. R-227ea in an amount of 3 wt. %

Based on the weight of the entire blend

Data were collected (Total BTUs and EER at any given minute) as the roomtemperature stabilized to 70° F. as the unit thermostat sat to.

Comparative tests were run on R-22 and R-417A and R-407C.

The ambient temperature was almost 82° F. (27.8° C.) during the tests ofall blends. Data were illustrated on Table 8-Table 11:

TABLE 8 (R-22 Test data) Reading Set Total Total AC AC No. point ReadWatts BTUs Volts Current Watts EER 1 70 70.5 2273 7750 245.8 3.6 8798.81 2 70 70.1 2267 7730 245.8 3.6 874 8.85 3 70 69.4 2263 7720 245.53.6 889 8.68 4 70 69.9 2263 7720 245.1 3.6 870 8.87 5 70 69.7 2288 7810245 3.6 873 8.95 6 70 69.7 2268 7740 244.8 3.6 869 8.91 Average 70.0069.88 2270.33 7745.00 245.33 3.60 875.67 8.85

TABLE 9 (R-417A Test data) Reading Set Total Total AC AC No. point ReadWatts BTUs Volts Current Watts EER 1 70 70.3 2025 6910 246.7 3.5 8518.12 2 70 70.1 2041 6960 246.8 3.4 834 8.34 3 70 69.7 2094 7140 247.93.4 847 8.43 4 70 69.3 2045 6980 246.8 3.3 819 8.52 5 70 69.5 2131 7270246.6 3.4 831 8.75 6 70 70.2 2112 7200 247.5 3.3 825 8.73 7 70 69.6 20336940 247 3.3 824 8.42 8 70 69.6 2066 7050 245.5 3.4 835 8.44 9 70 702291 7820 245.3 3.4 834 9.38 10 70 69.6 2294 7830 245.5 3.4 823 9.52 1170 70.2 1998 6820 246.2 3.3 802 8.51 12 70 69.9 1979 6750 245.4 3.4 8378.07 Average 70 69.83 2092.42 7139.17 246.43 3.38 830.17 8.60

TABLE 10 (R-407C Test data) Reading Set Total Total AC AC No. point ReadWatts BTUs Volts Current Watts EER 1 70 70.5 2011 6860 247.3 3.6 8987.64 2 70 70.2 2035 6940 246.9 3.6 889 7.81 3 70 70 2041 6960 246.9 3.6896 7.77 4 70 69.7 2049 6990 246.5 3.5 860 8.13 5 70 69.2 2056 7010 2473.6 892 7.86 6 70 69.2 2353 8030 246.8 3.5 870 9.23 7 70 69.6 2381 8120246.8 3.4 848 9.57 8 70 70 2357 8040 246.8 3.5 872 9.22 9 70 70.3 23177910 246.7 3.6 887 8.92 10 70 70.1 2324 7930 246.3 3.6 897 8.84 11 70 702293 7820 246.3 3.7 907 8.62 12 70 70.1 2279 7780 246.3 3.7 900 8.65Average 70.0 69.80 2267.67 7736.67 246.61 3.57 881.44 8.78

TABLE 11 (Refrigerant Blend) Reading Set Total Total AC AC No. pointRead Watts BTUs Volts Current Watts EER 1 70 70.60 2515 8580 246.7 3.5858 10 2 70 69.8 1968 6710 247.1 3.4 849 7.9 3 70 70.2 2155 7350 244.93.5 857 8.57 4 70 69.8 2279 7780 246.5 3.6 887 8.78 5 70 70 2262 7720246.2 3.5 869 8.88 6 70 69.5 2396 8180 246.7 3.5 855 9.56 7 70 69.7 24158240 246.3 3.5 870 9.47 8 70 70.4 2241 7650 246.6 3.5 856 8.93 9 70 69.72197 7490 244.8 3.6 877 8.54 10 70 69.4 2270 7750 245.3 3.6 871 8.9 1170 69.5 2302 7850 244.8 3.6 871 9.01 12 70 70.4 2285 7800 244.7 3.7 8948.72 13 70 70.6 2294 7830 245.6 3.6 879 8.9 14 70 70.4 2322 7920 246 3.6886 8.94 15 70 70.1 2334 7960 246.1 3.6 876 9.09 70.01 2282.33 7787.33245.89 3.55 870.33 8.95 Average 70 70.1 2282.33 7787.33 245.88 3.55870.33 8.90

As demonstrated by the above data and FIG. 3, it clearly when the unithas charged with the refrigerant blend it had capacity comparable withR-22 and better capacity compared to R-417A and R-407C. Also the a/cunit has less power consumption compared to all tested blends whichmeans has better efficiency (Total EER) FIG. 4.

It is to be understood that the above-described blends are merelyillustrative embodiments of the principles of the present disclosure,and that other compositions and methods for using same in refrigerationand air conditioning systems may be devised by those skilled in the art,without departing from the spirit and scope of the invention(s)disclosed herein. It is therefore intended that the foregoing detaileddescription be regarded as illustrative rather than limiting.

Example 3 R-125a/R-134a/R-143a/R-600/R-601/R-227A (65/7/22/1.5/1.5/3)

Ten (10) pounds refrigerant blend per the present invention was preparedwith the following percentages of components:

-   -   1. R-125a in an amount of 65 wt. %.    -   2. R-134a in an amount of 7 wt. %.    -   3. R-143a in an amount of 22 wt. %    -   4. R-600 in an amount of 1.5 wt. % AND R-601a in amount of 1.5        wt. %.    -   5. R-227ea in an amount of 3 wt. %

All based on the weight of the entire blend.

The blend charged into small charging cylinder which had been evacuatedto 100 microns of vacuum. The initial vacuum was sufficient to draw inthe hydro component (R-600 and R-601a) then R-227a. The chargingcylinder was next placed in freezer for 2 hours to lower the cylindertemperature the charging process continued in the sequence of R-134a,R-143a and finally R-125a.

After the components were added, the cylinder was shaken and rolled byhand to mix the components. The cylinder pressure was 135 PSIG at about72° F. was noted.

The charging cylinder was allowed to set overnight to make sure it wasstabilized. A quarter pound sample of the blend charged into smallstainless steel cylinder has a needle capillary tube allows dischargingthe refrigerant blend in vapor state (normally used in chromatographtesting machines).

A quick fractionation and flammability test was done by slowly vaporleaking out the charging sample through a needle valve (over a 20 minuteperiod). A propane torch flame was moved about the area of the leakingvapor to see if it could sustain ignition when the torch flame wasremoved. This test is not designed to replace the UL2182 or ASTM E681tests, but only to provide a quick check to whether the mixture isintroducing any ignite and if so there would be no point in doing theUL2182 test.

This sample didn't sustain ignition at the very beginning of the leakdown nor toward the end where the last drop of the refrigerant leakedout.

This is a good indication that this blend isn't flammable.

Example 4

A computer simulation with REFPROP V 6.0 indicates that the mixture ofExample 2 has bubble/dew pressures close to R-22 which would be goodalternative refrigerant to be used in comfort cooling systems speciallythe discharge pressures are close in matching R-22 which will not causedamages to the compressor after long usage, also it has better mineraloil return compared to R-417A and other R-22 alternatives and that isdue to the small amount of the hydro component (only 3%).

Unlike R-417A, which has about 22 percent reduced capacity compared toR-22.

Blend of example 2 would be close in matching R-22 in capacity andefficiency.

Example 5 R-125a/R-134a/R-143a/R-600/R-601/R-227A (65/7/22/1.5/1.5/3)

-   -   1. R-125a in an amount of 65 wt. %.    -   2. R-134a in an amount of 7 wt. %.    -   3. R-143a in an amount of 22 wt. %    -   4. R-600 in an amount of 1.5 wt. % AND R-601a in amount of 1.5        wt. %.    -   5. R-227ea in an amount of 3 wt. %

Based on the weight of the entire blend.

A computer simulation with RERPROP V6.0 indicates that the mixture ofExample 1 would be a close match to replace R-22, R-404A, and R-502, seeTable 11.

TABLE 12 (Refrigerant pressures Vs. Temperatures) 0° F. 32° F. 70° F.130° F. Blended 21.00 42.10 86.60 214.02 sample psi R-22 21.16 42.4585.75 214.75 R-404A 22.60 45.04 90.62 224.90 R-502 27.22 50.60 98.22227.75

Although the pressures may be slightly higher than R-404A, it shouldstill work in most cases and provide some increase in capacity. This isespecially useful in display refrigerators and freezers were it may beless expensive to use example 1 blend refrigerant compared to any othersystem using POE oil.

What is claimed is:
 1. A refrigerant mixture, comprising:Pentafluoroethane (HFC-125) comprising between about 35 to 65 weightpercent; 1,1,1,2-Tetrafluoroethane (HFC-134a) comprising between about20 to 55 weight percent; 1,1,1-Trifluoroethane (HFC-143a) comprisingbetween about 5 to 25 weight percent; one or more hydrocarbon componentscomprising about 1 to 5 weight percent; and1,1,2,3,3,3-Heptafluoropropane (HFC-227ea) comprising between about 2 to10 weight percent.
 2. The refrigerant mixture of claim 1, wherein eachweight percent represents its respective weight percentage of therefrigerant mixture.
 3. The refrigerant mixture of claim 1, wherein therefrigerant mixture comprises a substitute for chlorodifluoromethane inrefrigerant applications.
 4. The refrigerant mixture of claim 1,wherein: the Pentafluoroethane (HFC-125) comprises about 65 weightpercent; the 1,1,1,2-Tetrafluoroethane (HFC-134a) comprises about 7weight percent; the 1,1,1-Trifluoroethane (HFC-143a) comprises about 22weight percent; the one or more hydrocarbon components comprises about 3weight percent; and the 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea)comprises about 3 weight percent.
 5. The refrigerant mixture of claim 1,wherein the one or more hydrocarbon components are selected from thegroup comprising: R-600, R-601, and R-601a.
 6. A refrigerant mixture,comprising: Pentafluoroethane (HFC-125) comprising between about 45 to75 weight percent; 1,1,1,2-Tetrafluoroethane (HFC-134a) comprisingbetween about 5 to 20 weight percent; 1,1,1, Trifluoroethane (HFC-143a)comprising between about 10 to 40 weight percent;1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea) comprising between about 2to 10 weight percent; and at least one hydrocarbon component comprisingbetween about 1 to 5 weight percent.
 7. The refrigerant mixture of claim6, wherein each weight percent represents its respective weightpercentage of the refrigerant mixture.
 8. The refrigerant mixture ofclaim 6, wherein the refrigerant mixture comprises a substitute for oneor more of the following refrigerant blends: R-502, R-404A, R-402A,R-402B, R-404A, R-408A, R-407C, R-502 and R-507A.
 9. The refrigerantmixture of claim 8, wherein the R502 comprises chlorodifluoromethanecomprising about 48.8 weight percent and chloropentafluoroethanecomprising about 51.2 weight percent.
 10. The refrigerant mixture ofclaim 8, wherein the R404A comprises pentafluoroethane comprising about44 weight percent, 1,1,1-trifluoroethane comprising about 52 weightpercent, and 1,1,1,2-tetrafluoroethane comprising about 4 weightpercent.
 11. The refrigerant mixture of claim 6, wherein: thePentafluoroethane (HFC-125) comprises about 65 weight percent; the1,1,1,2-Tetrafluoroethane (HFC-134a) comprises about 7 weight percent;the 1,1,1-Trifluoroethane (HFC-143a) comprises about 22 weight percent;the 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea) comprises about 3weight percent; and the at least one hydrocarbon component comprisesabout 3 weight percent.
 12. The refrigerant mixture of claim 6, whereinthe at least one hydrocarbon component is selected from the groupcomprising: R-600, R-601, R-601a.
 13. A method for producingrefrigeration in a refrigeration system designed forchlorodifluoromethane refrigerant, comprising the steps of: obtaining apredetermined amount of chlorodifluoromethane refrigerant; substitutingfor the predetermined amount of chlorodifluoromethane refrigerant amixture comprising the following components: Pentafluoroethane (HFC-125)comprising between about 35 to 65 weight percent of the mixture;1,1,1,2-Tetrafluoroethane (HFC-134a) comprising between about 20 to 55weight percent of the mixture; 1,1,1, Trifluoroethane (HFC-143a)comprising between about 5 to 7 weight percent of the mixture;1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea) comprising between about 1to 5 weight percent of the mixture; and at least one hydrocarboncomponent comprising between about 1 to 5 weight percent of the mixture.14. The method of claim 13, wherein: the Pentafluoroethane (HFC-125)comprises about 55 weight percent; the 1,1,1,2-Tetrafluoroethane(HFC-134a) comprises about 32 weight percent; the 1,1,1, Trifluoroethane(HFC-143a) comprises about 7 weight percent; the1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea) comprises about 3 weightpercent; and the at least one hydrocarbon component comprises about 3weight percent.
 15. A method for using a substitute refrigerant blend ina refrigeration system, comprising the steps of: obtaining apredetermined amount of one of the following refrigerants: R-502,R-404A, R-402A, R-402B, R-404A, R-408A, R-407C, R-502 and R-507A,substituting for the predetermined amount of refrigerant a mixturecomprising the following components: Pentafluoroethane (HFC-125)comprising between about 45 to 75 weight percent of the mixture;1,1,1,2-Tetrafluoroethane (HFC-134a) comprising between about 5 to 20weight percent of the mixture; 1,1,1, Trifluoroethane (HFC-143a)comprising between about 10 to 40 weight percent of the mixture;1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea) comprising between about 2to 10 weight percent of the mixture; and at least one hydrocarboncomponent comprising between about 1 to 5 weight percent of the mixture.16. The method of claim 15, wherein the R502 compriseschlorodifluoromethane comprising about 48.8 weight percent andchloropentafluoroethane comprising about 51.2 weight percent.
 17. Themethod of claim 15, wherein the R404A comprises pentafluoroethanecomprising about 44 weight percent, 1,1,1-trifluoroethane comprisingabout 52 weight percent, and 1,1,1,2-tetrafluoroethane comprising about4 weight percent.
 18. The method of claim 15 wherein: thePentafluoroethane (HFC-125) comprises about 65 weight percent; the1,1,1,2-Tetrafluoroethane (HFC-134a) comprises about 7 weight percent;the 1,1,1-Trifluoroethane (HFC-143a) comprises about 22 weight percent;the 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea) comprises about 3weight percent; and the at least one hydrocarbon component comprisesabout 3 weight percent.
 19. The method of claim 15, wherein the at leastone hydrocarbon component is selected from the group comprising: R-600,R-601, and R-601a.